CN106839177A - Interstage flow heat exchanger and the solution humidifying unit with it - Google Patents
Interstage flow heat exchanger and the solution humidifying unit with it Download PDFInfo
- Publication number
- CN106839177A CN106839177A CN201710168163.4A CN201710168163A CN106839177A CN 106839177 A CN106839177 A CN 106839177A CN 201710168163 A CN201710168163 A CN 201710168163A CN 106839177 A CN106839177 A CN 106839177A
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- China
- Prior art keywords
- heat exchanger
- fluid passage
- flow heat
- import
- outlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 239000012530 fluid Substances 0.000 claims abstract description 82
- 239000007788 liquid Substances 0.000 claims abstract description 55
- 238000009938 salting Methods 0.000 claims abstract description 50
- 230000008929 regeneration Effects 0.000 claims abstract description 46
- 238000011069 regeneration method Methods 0.000 claims abstract description 46
- 230000008676 import Effects 0.000 claims abstract description 41
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 4
- 238000009421 internal insulation Methods 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 238000005057 refrigeration Methods 0.000 abstract description 6
- 239000000243 solution Substances 0.000 description 38
- 239000012266 salt solution Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 4
- 125000004122 cyclic group Chemical group 0.000 description 3
- 238000013016 damping Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F3/1411—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
- F24F3/1417—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with liquid hygroscopic desiccants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/30—Arrangement or mounting of heat-exchangers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F3/00—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
- F24F3/12—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
- F24F3/14—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
- F24F2003/1458—Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification using regenerators
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Central Air Conditioning (AREA)
Abstract
The invention provides a kind of interstage flow heat exchanger and the solution humidifying unit with it, interstage flow heat exchanger includes：There is first fluid passage and second fluid passage in heat exchanger, heat exchanger；Wherein, first fluid passage has the first import and first outlet, and positioned at solution humidifying machine except wet tank, first outlet is located at the regeneration case of solution humidifying machine for the first import, so that except the salting liquid of wet tank flows into regeneration case after first fluid passage；Second fluid passage has the second import and second outlet, and the second import is used to be connected with the salting liquid return line of regeneration case, and second outlet is located at except in wet tank, so that the salting liquid in salting liquid return line is flowed into except wet tank after second fluid passage.Interstage flow heat exchanger of the invention solves the problems, such as that the loss of refrigeration capacity of solution humidifying unit of the prior art is more serious.
Description
Technical field
The present invention relates to solution humidifying field, in particular to a kind of interstage flow heat exchanger and the solution with it adjust
Wet unit.
Background technology
In solution humidifying unit running process, due to being gradually reduced except wet side concentration of salt solution, regeneration side salting liquid is dense
Degree gradually increases so that unit finally loses damping ability.
In order to maintain both sides concentration of salt solution to be basically unchanged, solution humidifying unit is continuously run, it is necessary to be passed through to except wet side
High concentration salt solutions, regeneration side is passed through low concentration salt solution.However, because high concentration salt solutions temperature is higher, low concentration of salt is molten
Liquid temperature degree is relatively low, directly mixes, and can cause loss of refrigeration capacity.
The content of the invention
It is a primary object of the present invention to provide a kind of interstage flow heat exchanger and solution humidifying unit with it, to solve
The more serious problem of the loss of refrigeration capacity of solution humidifying unit of the prior art.
To achieve these goals, according to an aspect of the invention, there is provided a kind of interstage flow heat exchanger, including：Heat
There is first fluid passage and second fluid passage in exchanger, heat exchanger；Wherein, first fluid passage has the first import
And first outlet, positioned at solution humidifying machine except wet tank, first outlet is located at the regeneration case of solution humidifying machine for the first import, so that
Except the salting liquid of wet tank flows into regeneration case after first fluid passage；Second fluid passage has the second import and second outlet,
Second import is used to be connected with the salting liquid return line of regeneration case, and second outlet is located at except in wet tank, so that salting liquid flows back
Salting liquid in pipeline is flowed into except wet tank after second fluid passage.
Further, heat exchanger also includes：Housing, first fluid passage and second fluid passage are arranged at housing
In cavity, first fluid passage and second fluid passage extend along the bearing of trend of housing.
Further, housing is pipe structure, and the first import and first outlet are separately positioned on the end at pipe structure two ends
At mouthful, the second import and second outlet are separately positioned on the side wall at pipe structure two ends.
Further, heat exchanger also includes：Body, body is arranged in the cavity of housing, and the first import and first goes out
Mouth is respectively two mouths of pipe of body, the segment dislocation first fluid passage of body；Wherein, the inwall of the outer wall of body and housing
The gap for being surrounded into forms second fluid passage.
Further, body is multiple, and multiple bodys are abreast arranged at enclosure interior to form Pipe bundle structure.
Further, body is titanium tube.
Further, housing is pipe structure, has been blocked at two mouths of pipe of pipe structure for by extraneous and body
The end plate of the internal insulation of structure；The two ends of body pass from each end plate respectively.
Further, heat exchanger also includes：Spoiler, spoiler is arranged on enclosure interior, and spoiler is located at second
Body channel interior.
Further, spoiler is multiple, and multiple spoilers are positioned apart from along the bearing of trend of second fluid passage.
According to another aspect of the present invention, there is provided a kind of solution humidifying unit, be included in regeneration case, except wet tank and with
Regeneration case and the interstage flow heat exchanger connected except wet tank, interstage flow heat exchanger is above-mentioned interstage flow heat exchanger.
Interstage flow heat exchanger of the invention by be disposed at solution humidifying machine except wet tank and solution humidifying machine again
Between raw case, by the first fluid passage and second fluid passage of heat exchanger realize solution humidifying unit except wet side with
Regenerate the mixing of side salting liquid.For the cyclic process of concrete structure and salting liquid, wherein, first fluid passage has first
Import and first outlet, positioned at solution humidifying machine except wet tank, first outlet is located at the regeneration case of solution humidifying machine for the first import,
So that except the salting liquid of wet tank flows into regeneration case after first fluid passage；There is second fluid passage the second import and second to go out
Mouthful, the second import is used to be connected with the salting liquid return line of regeneration case, and second outlet is located at except in wet tank, so that salting liquid is returned
Salting liquid in flow tube road is flowed into except wet tank after second fluid passage；By in solution humidifying machine except wet tank and solution humidifying
Interstage flow heat exchanger is set between the regeneration case of machine, is first made the high temperature in regeneration case, high concentration salt solutions and is removed low in wet tank
Temperature, low concentration salt solution exchanged heat in the second fluid passage and first fluid passage of interstage flow heat exchanger, then respectively with remove
Wet tank mixes with the salting liquid in regeneration case, so as to the loss of refrigeration capacity for solving solution humidifying unit of the prior art is more tight
The problem of weight.
Brief description of the drawings
The Figure of description for constituting the part of the application is used for providing a further understanding of the present invention, of the invention to show
Meaning property and its illustrates, for explaining the present invention, not constitute inappropriate limitation of the present invention embodiment.In the accompanying drawings：
Fig. 1 shows the structural representation of the embodiment of interstage flow heat exchanger use state of the invention；And
Fig. 2 shows the front view of interstage flow heat exchanger of the invention.
Wherein, above-mentioned accompanying drawing is marked including the following drawings：
10th, heat exchanger；11st, the first import；12nd, first outlet；13rd, the second import；14th, second outlet；20th, housing；
30th, body；40th, end plate；50th, connecting tube；60th, except wet tank；70th, case is regenerated.
Specific embodiment
It should be noted that in the case where not conflicting, the feature in embodiment and embodiment in the application can phase
Mutually combination.Describe the present invention in detail below with reference to the accompanying drawings and in conjunction with the embodiments.
The invention provides a kind of interstage flow heat exchanger, Fig. 1 and Fig. 2 is refer to, interstage flow heat exchanger includes：Heat exchanger
10, there is first fluid passage and second fluid passage in heat exchanger 10；Wherein, first fluid passage has the first import 11
With first outlet 12, positioned at solution humidifying machine except wet tank 60, first outlet 12 is located at solution humidifying machine again for the first import 11
Raw case 70, so that except the salting liquid of wet tank 60 flows into regeneration case 70 after first fluid passage；Second fluid passage has second
Import 13 and second outlet 14, the second import 13 are used to be connected with the salting liquid return line of regeneration case 70, second outlet 14
In except wet tank 60, so that the salting liquid in salting liquid return line is flowed into except wet tank 60 after second fluid passage.
Interstage flow heat exchanger of the invention by be disposed at solution humidifying machine except wet tank 60 and solution humidifying machine
Between regeneration case 70, removing for solution humidifying unit is realized by the first fluid passage and second fluid passage of heat exchanger 10
Wet side and the mixing for regenerating side salting liquid.For the cyclic process of concrete structure and salting liquid, wherein, first fluid passage tool
There are the first import 11 and first outlet 12, positioned at solution humidifying machine except wet tank 60, first outlet 12 is located at molten for the first import 11
The regeneration case 70 of liquid damping machine, so that except the salting liquid of wet tank 60 flows into regeneration case 70 after first fluid passage；Second fluid
Passage has the second import 13 and second outlet 14, and the second import 13 is used to be connected with the salting liquid return line of regeneration case 70,
Second outlet 14 is located at except in wet tank 60, so that the salting liquid in salting liquid return line flows into dehumidifying after second fluid passage
Case 60；By solution humidifying machine except between wet tank 60 and the regeneration case 70 of solution humidifying machine set interstage flow heat exchanger, first
Make the high temperature in regeneration case 70, high concentration salt solutions with low temperature, the low concentration salt solution removed in wet tank 60 in interstage flow heat exchanger
Second fluid passage and first fluid passage in heat exchange, then respectively with except wet tank 60 with regeneration case 70 in salting liquid mix
Close, so as to the loss of refrigeration capacity for solving the problems, such as solution humidifying unit of the prior art is more serious.
In view of first fluid passage and the sealing of second fluid passage, heat exchanger 10 also includes：Housing 20, first
Fluid passage and second fluid passage are arranged in the cavity of housing 20, and first fluid passage and second fluid passage are along shell
The bearing of trend of body 20 extends.
Preferably, housing 20 is pipe structure, and the first import 11 and first outlet 12 are separately positioned on pipe structure two ends
Port, the second import 13 and second outlet 14 are separately positioned on the side wall at pipe structure two ends.Wherein, the second import 13
Connected with salting liquid return line by connecting tube 50.
In order to ensure solution humidifying unit except wet side with regeneration side salting liquid can effectively pass through first fluid passage
Mixed with second fluid, heat exchanger 10 also includes：Body 30, body 30 is arranged in the cavity of housing 20, and first enters
Mouth 11 and first outlet 12 are respectively two mouths of pipe of body 30, the segment dislocation first fluid passage of body 30；Wherein, body
The gap that 30 outer wall and the inwall of housing 20 are surrounded into forms second fluid passage.
In the present embodiment, by being provided with body 30 on heat exchanger 10, wherein, body 30 is arranged at housing 20
In cavity, two mouths of pipe of the first import 11 and the respectively body 30 of first outlet 12, the segment dislocation first fluid of body 30
Passage；The gap that the outer wall of body 30 and the inwall of housing 20 are surrounded into forms second fluid passage.
Preferably, body 30 is multiple, and multiple bodys 30 are abreast arranged inside housing 20 to form Pipe bundle structure.
Preferably, body 30 is titanium tube.
In order to realize the fixation to body 30, housing 20 is pipe structure, has been blocked at two mouths of pipe of pipe structure
For by the end plate 40 of the extraneous internal insulation with pipe structure；The two ends of body 30 pass from each end plate 40 respectively.At this
In embodiment, by blocking at two mouths of pipe of pipe structure for by the end of the extraneous internal insulation with pipe structure
Plate 40, the two ends of body 30 pass from each end plate 40 respectively, and body 30 is fixedly installed on inside housing 20 with this.
In order to strengthen the heat-transfer effect of second fluid channel interior, heat exchanger 10 also includes：Spoiler, spoiler is set
Inside housing 20, spoiler is located at second fluid channel interior.Spoiler is provided with by heat exchanger 10, wherein,
Spoiler is arranged on inside housing 20, and second fluid passage can be strengthened by the way that spoiler is arranged at into second fluid channel interior
Internal heat-transfer effect.
Preferably, spoiler is multiple, and multiple spoilers are positioned apart from along the bearing of trend of second fluid passage.
Present invention also offers a kind of solution humidifying unit, be included in regeneration case 70, except wet tank 60 and with regeneration case 70
With the interstage flow heat exchanger connected except wet tank 60, interstage flow heat exchanger is above-mentioned interstage flow heat exchanger.
Concrete structure and operation principle for interstage flow heat exchanger of the invention are illustrated：
Wherein, interstage flow heat exchanger is made up of tube bank, end plate 40, spoiler, housing 20.Housing 20 is ABS plastic pipe, interior
Portion has titanium tube to restrain, tube bank two ends fixed by end plate 40, after it is Nian Jie with plastic casing.It is reinforcing tube bank outside heat transfer,
Multiple spoilers are installed, spoiler is semicircle spoiler in housing.
The both sides of body 30 of interstage flow heat exchanger connect respectively with regeneration side (high temperature), except wet side (low temperature) salting liquid.Change
Hot device lateral opening hole, one end design pipeline connection regeneration side high temperature salt solution backflow pipe road, the other end is immersed in except wet side is (low
Temperature) in salting liquid.(first fluid passage) manages outer (second fluid passage) again except wet side low temperature salting liquid flow direction regeneration side in pipe
Raw side reflux salting liquid flow direction removes wet side.
In the case where heat exchanger both sides salting liquid liquid level difference drives, low temperature salting liquid makes regeneration side molten through flow direction regeneration side in pipe
Liquid concentration is held essentially constant.Heat exchanger side one end perforate (the second import 13) connection regeneration side (high temperature) salting liquid return duct
Road, the other end only needs perforate (second outlet 14) to be immersed in except in wet side (low temperature) salting liquid.Backflow high temperature salting liquid with it is low
Under the thermohaline solution discrepancy in elevation drives, high temperature salting liquid flows into dehumidifying side through pipe is outer, maintains to be basically unchanged except wet side solution concentration.
As can be seen from the above description, the above embodiments of the present invention realize following technique effect：
Interstage flow heat exchanger of the invention by be disposed at solution humidifying machine except wet tank 60 and solution humidifying machine
Between regeneration case 70, removing for solution humidifying unit is realized by the first fluid passage and second fluid passage of heat exchanger 10
Wet side and the mixing for regenerating side salting liquid.For the cyclic process of concrete structure and salting liquid, wherein, first fluid passage tool
There are the first import 11 and first outlet 12, positioned at solution humidifying machine except wet tank 60, first outlet 12 is located at molten for the first import 11
The regeneration case 70 of liquid damping machine, so that except the salting liquid of wet tank 60 flows into regeneration case 70 after first fluid passage；Second fluid
Passage has the second import 13 and second outlet 14, and the second import 13 is used to be connected with the salting liquid return line of regeneration case 70,
Second outlet 14 is located at except in wet tank 60, so that the salting liquid in salting liquid return line flows into dehumidifying after second fluid passage
Case 60；By solution humidifying machine except between wet tank 60 and the regeneration case 70 of solution humidifying machine set interstage flow heat exchanger, first
Make the high temperature in regeneration case 70, high concentration salt solutions with low temperature, the low concentration salt solution removed in wet tank 60 in interstage flow heat exchanger
Second fluid passage and first fluid passage in heat exchange, then respectively with except wet tank 60 with regeneration case 70 in salting liquid mix
Close, so as to the loss of refrigeration capacity for solving the problems, such as solution humidifying unit of the prior art is more serious.
The preferred embodiments of the present invention are the foregoing is only, is not intended to limit the invention, for the skill of this area
For art personnel, the present invention can have various modifications and variations.It is all within the spirit and principles in the present invention, made any repair
Change, equivalent, improvement etc., should be included within the scope of the present invention.
Claims (10)
1. a kind of interstage flow heat exchanger, it is characterised in that including：
There is first fluid passage and second fluid passage in heat exchanger (10), the heat exchanger (10)；
Wherein, the first fluid passage has the first import (11) and first outlet (12), and first import (11) is located at
Solution humidifying machine except wet tank (60), the first outlet (12) positioned at the solution humidifying machine regeneration case (70) so that institute
State except the salting liquid of wet tank (60) flows into regeneration case (70) after the first fluid passage；
The second fluid passage have the second import (13) and second outlet (14), second import (13) for it is described
The salting liquid return line connection of regeneration case (70), the second outlet (14) positioned at described except in wet tank (60) so that described
Salting liquid in salting liquid return line flows into described except wet tank (60) after the second fluid passage.
2. interstage flow heat exchanger according to claim 1, it is characterised in that the heat exchanger (10) also includes：
Housing (20), the first fluid passage and the second fluid passage are arranged in the cavity of the housing (20),
The first fluid passage and the second fluid passage extend along the bearing of trend of the housing (20).
3. interstage flow heat exchanger according to claim 2, it is characterised in that the housing (20) is pipe structure, described
First import (11) and the first outlet (12) are separately positioned on the port at the pipe structure two ends, second import
(13) it is separately positioned on the side wall at the pipe structure two ends with the second outlet (14).
4. interstage flow heat exchanger according to claim 2, it is characterised in that the heat exchanger (10) also includes：
Body (30), the body (30) is arranged in the cavity of the housing (20), first import (11) and described
One outlet (12) is respectively two mouths of pipe of the body (30), and first fluid described in the segment dislocation of the body (30) leads to
Road；Wherein, the gap that the outer wall of the body (30) and the inwall of the housing (20) are surrounded into forms the second fluid
Passage.
5. interstage flow heat exchanger according to claim 4, it is characterised in that the body (30) is multiple, it is multiple described
It is internal to form Pipe bundle structure that body (30) is abreast arranged at the housing (20).
6. interstage flow heat exchanger according to claim 5, it is characterised in that the body (30) is titanium tube.
7. the interstage flow heat exchanger according to any one of claim 4 to 6, it is characterised in that the housing (20) is pipe
Body structure, blocks for by the end of the external world and the internal insulation of the pipe structure at two mouths of pipe of the pipe structure
Plate (40)；The two ends of the body (30) pass from each end plate (40) respectively.
8. interstage flow heat exchanger according to claim 2, it is characterised in that the heat exchanger (10) also includes：
Spoiler, the spoiler is arranged on the housing (20) inside, and the spoiler is located in the second fluid passage
Portion.
9. interstage flow heat exchanger according to claim 8, it is characterised in that the spoiler is multiple, disturbs described in multiple
Stream plate is positioned apart from along the bearing of trend of the second fluid passage.
10. a kind of solution humidifying unit, be included in regeneration case (70), except wet tank (60) and with regeneration case (70) and described
Except the interstage flow heat exchanger that wet tank (60) is connected, it is characterised in that the interstage flow heat exchanger is in claim 1 to 9
Interstage flow heat exchanger described in one.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710168163.4A CN106839177A (en) | 2017-03-20 | 2017-03-20 | Interstage flow heat exchanger and the solution humidifying unit with it |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710168163.4A CN106839177A (en) | 2017-03-20 | 2017-03-20 | Interstage flow heat exchanger and the solution humidifying unit with it |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106839177A true CN106839177A (en) | 2017-06-13 |
Family
ID=59130253
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710168163.4A Pending CN106839177A (en) | 2017-03-20 | 2017-03-20 | Interstage flow heat exchanger and the solution humidifying unit with it |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106839177A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2009090979A (en) * | 2008-11-25 | 2009-04-30 | National Institute Of Advanced Industrial & Technology | Small desiccant air conditioner |
| CN101512238A (en) * | 2006-08-25 | 2009-08-19 | 阿迪尔西格尔有限公司 | System and method for managing water content in a fluid |
| CN102149980A (en) * | 2008-08-08 | 2011-08-10 | 技术研究及发展基金有限公司 | Liquid desiccant dehumidification system and heat /mass exchanger therefor |
| CN102425832A (en) * | 2011-11-28 | 2012-04-25 | 同济大学 | Air conditioning method and air conditioning system based on directly utilizing solar-ground heat |
| CN203454867U (en) * | 2013-06-19 | 2014-02-26 | 中冶南方工程技术有限公司 | Highly-corrosive resistant shell and tube heat exchanger |
| CN106440883A (en) * | 2016-12-06 | 2017-02-22 | 无锡优耐特净化装备有限公司 | Horizontal type shell-and-tube heat exchanger |
| CN206618051U (en) * | 2017-03-20 | 2017-11-07 | 北京华创瑞风空调科技有限公司 | Interstage flow heat exchanger and the solution humidifying unit with it |
-
2017
- 2017-03-20 CN CN201710168163.4A patent/CN106839177A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101512238A (en) * | 2006-08-25 | 2009-08-19 | 阿迪尔西格尔有限公司 | System and method for managing water content in a fluid |
| CN102149980A (en) * | 2008-08-08 | 2011-08-10 | 技术研究及发展基金有限公司 | Liquid desiccant dehumidification system and heat /mass exchanger therefor |
| JP2009090979A (en) * | 2008-11-25 | 2009-04-30 | National Institute Of Advanced Industrial & Technology | Small desiccant air conditioner |
| CN102425832A (en) * | 2011-11-28 | 2012-04-25 | 同济大学 | Air conditioning method and air conditioning system based on directly utilizing solar-ground heat |
| CN203454867U (en) * | 2013-06-19 | 2014-02-26 | 中冶南方工程技术有限公司 | Highly-corrosive resistant shell and tube heat exchanger |
| CN106440883A (en) * | 2016-12-06 | 2017-02-22 | 无锡优耐特净化装备有限公司 | Horizontal type shell-and-tube heat exchanger |
| CN206618051U (en) * | 2017-03-20 | 2017-11-07 | 北京华创瑞风空调科技有限公司 | Interstage flow heat exchanger and the solution humidifying unit with it |
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Application publication date: 20170613 |
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